JPH0384867A - Fuel cell - Google Patents
Fuel cellInfo
- Publication number
- JPH0384867A JPH0384867A JP1218534A JP21853489A JPH0384867A JP H0384867 A JPH0384867 A JP H0384867A JP 1218534 A JP1218534 A JP 1218534A JP 21853489 A JP21853489 A JP 21853489A JP H0384867 A JPH0384867 A JP H0384867A
- Authority
- JP
- Japan
- Prior art keywords
- plate
- separator
- current collector
- anode
- corrosion
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000000446 fuel Substances 0.000 title claims description 17
- 238000005452 bending Methods 0.000 claims abstract description 7
- 238000005260 corrosion Methods 0.000 claims description 26
- 239000007789 gas Substances 0.000 claims description 17
- 210000002105 tongue Anatomy 0.000 claims description 16
- 239000003792 electrolyte Substances 0.000 claims description 8
- 239000002737 fuel gas Substances 0.000 claims description 7
- 230000001590 oxidative effect Effects 0.000 claims description 6
- 238000000034 method Methods 0.000 abstract description 8
- 230000000873 masking effect Effects 0.000 abstract description 4
- 238000005520 cutting process Methods 0.000 abstract description 2
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 9
- 230000007797 corrosion Effects 0.000 description 6
- 230000005611 electricity Effects 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 4
- 229910052782 aluminium Inorganic materials 0.000 description 4
- CIWBSHSKHKDKBQ-JLAZNSOCSA-N Ascorbic acid Chemical compound OC[C@H](O)[C@H]1OC(=O)C(O)=C1O CIWBSHSKHKDKBQ-JLAZNSOCSA-N 0.000 description 3
- 229910000831 Steel Inorganic materials 0.000 description 3
- 239000011248 coating agent Substances 0.000 description 3
- 238000000576 coating method Methods 0.000 description 3
- 239000010959 steel Substances 0.000 description 3
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000009792 diffusion process Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229910052744 lithium Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 238000005536 corrosion prevention Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229910000859 α-Fe Inorganic materials 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
Landscapes
- Fuel Cell (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は燃料の有する化学エネルギーを直接電気エネル
ギーに変換させるエネルギ一部門で用いる燃料電池、特
に、溶融炭酸塩型燃料電池に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to fuel cells used in the energy sector for directly converting the chemical energy of fuel into electrical energy, and in particular to molten carbonate fuel cells.
[従来の技術]
従来の溶融炭酸塩型燃料電池は、第3図に一例の概略を
示す如く、電解質として溶融炭酸塩を多孔質物質にしみ
込ませてなる電解質板(タイル)1を、カソード(酸素
極)2とアノード(燃料極〉3の両電極で両面から挟み
、カソード2側に酸化ガスOGを供給すると共にアノー
ド3側に燃料ガスFGを供給することにより、カソード
2側での反応で得られた炭酸イオンCO3°−が電解質
板1中を通して7ノード3へと導かれ、アノード3側で
燃料ガスとの反応が行われて、カソード2とアノード3
との間で発生する電位差により発電が行われるようにし
たものを1セルCとし、各セルをセパレータ4を介して
多層に積層させてスタックとするようにしてある。[Prior Art] A conventional molten carbonate fuel cell, as shown schematically in FIG. By sandwiching the oxygen electrode (oxygen electrode) 2 and the anode (fuel electrode) 3 from both sides, and supplying the oxidizing gas OG to the cathode 2 side and the fuel gas FG to the anode 3 side, the reaction on the cathode 2 side The obtained carbonate ions CO3°- are guided through the electrolyte plate 1 to the 7 node 3, and react with the fuel gas on the anode 3 side, causing the cathode 2 and the anode 3 to react.
One cell C is configured to generate electricity by the potential difference generated between the two cells, and each cell is laminated in multiple layers with a separator 4 in between to form a stack.
かかる溶融炭酸塩型燃料電池で用いられるセパレータ4
としては、センタープレート5の両面側にコルゲート板
6を重ね合わせ、コルゲート板6の凹凸によりガス通路
を形成させるようにしたものが提案されており、センタ
ープレート5の両面のコルゲート板6の波のピッチが広
い場合は、電極の変形防止と、電極の電解質板1への−
様な接触確保とを図るためにパンチ板7をコルゲート板
6の外側に組み合わせて用いるようにし、該パンチ板γ
をカレントコレクターとしている。Separator 4 used in such a molten carbonate fuel cell
It has been proposed that corrugated plates 6 are stacked on both sides of the center plate 5, and gas passages are formed by the unevenness of the corrugated plates 6. If the pitch is wide, prevent deformation of the electrodes and -
In order to ensure various contact, a punch plate 7 is used in combination on the outside of the corrugated plate 6, and the punch plate γ
is used as the current collector.
[発明が解決しようとする課題]
ところが、溶融炭酸塩型燃料電池では、その作動温度が
600〜700℃と高く且つ腐食性の強い溶融炭酸塩中
で酸化、還元雰囲気の両方にセパレータはさらされてい
る関係上、セパレータは腐食し易く、セパレータの腐食
が進行すると、溶融炭酸塩中のリチウムが消費されると
同時に接触抵抗が増大し、電池の寿命が低下する。その
ため、セパレータに防食性をもたせることが必要である
が、従来の燃料電池では、セパレータの母材そのものに
防食性のあるものを使い、特別に防食処理を施こすこと
は行っていなかった。[Problems to be Solved by the Invention] However, in molten carbonate fuel cells, the operating temperature is as high as 600 to 700°C, and the separator is exposed to both oxidizing and reducing atmospheres in molten carbonate, which is highly corrosive. Because of this, the separator is prone to corrosion, and as the separator corrosion progresses, lithium in the molten carbonate is consumed and at the same time contact resistance increases, reducing the battery life. Therefore, it is necessary for the separator to have anti-corrosion properties, but in conventional fuel cells, the base material of the separator itself is made of a material that has anti-corrosion properties, and no special anti-corrosion treatment is applied.
そこで、本発明は、片面に防食処理を施こしたものに多
数の折曲げ加工部と孔を形成して同時にガス通路を形成
させたものをカレントコレクターとする燃料電池を提供
しようとするものである。SUMMARY OF THE INVENTION Therefore, the present invention aims to provide a fuel cell in which a current collector is formed by applying anti-corrosion treatment on one side and forming a large number of bent parts and holes to simultaneously form gas passages. be.
[課題を解決するための手段]
本発明は、上記課題を解決するために、電解質板をカソ
ードとアノードの両電極で両面から挟み、カソード側に
酸化ガスを、又、アノード側に燃料ガスをそれぞれ供給
するようにしてあるセルをセパレータを介して多層に積
層させる燃料電池において、片面側に防食処理を施こし
た1枚のプレートの多数個所に、コの字形に切込み部を
設けて、該各切込み部の舌片を片面側の方向へ折曲げ加
工してなるカレントコレクターを構成し、該カレントコ
レクターの上記片面側をセパレータプレートに当接させ
て、セパレータプレートとカレントコレクターとの間に
折曲舌片によるガス通路を形成させた構成とする。[Means for Solving the Problems] In order to solve the above problems, the present invention sandwiches an electrolyte plate between both electrodes, a cathode and an anode, and supplies oxidizing gas to the cathode side and fuel gas to the anode side. In a fuel cell in which cells are stacked in multiple layers via separators, each plate is coated with anti-corrosion treatment on one side, and U-shaped notches are provided at multiple locations. A current collector is constructed by bending the tongue piece of each cut portion toward one side, and the one side of the current collector is brought into contact with a separator plate, and the tongue is folded between the separator plate and the current collector. It has a configuration in which a gas passage is formed by a curved tongue piece.
又、上記プレートへの防食処理の方法としては、片面に
アルミニウム等をコーティングする方法、母材としての
1枚のプレートとアルミニウム等を拡散接合させてクラ
ツド鋼とする方法がある。In addition, methods for applying anti-corrosion treatment to the plate include a method of coating one side with aluminum or the like, or a method of diffusion bonding one plate as a base material and aluminum or the like to form clad steel.
[作 用1
防食処理をした1枚のプレートの多数個所に切り込みに
より形成した舌片を片面側へ折り曲げることにより同時
に多数の孔が形成されるので、パンチ板として機能し、
又、折り曲げた舌片をセパレータプレートに当接させる
ことによりガス通路が形成される。これにより従来のコ
ルゲート板を省略することができる。又、防食処理は1
枚板のときに行うので、加工後に防食処理を行う場合に
比してコーティングの際のマスキングの工程を省くこと
ができる。[Function 1] A large number of holes are simultaneously formed by cutting tongues formed in multiple places on one anti-corrosion plate and bending them to one side, so it functions as a punch plate.
Further, a gas passage is formed by bringing the bent tongue piece into contact with the separator plate. This allows the conventional corrugated board to be omitted. In addition, the anti-corrosion treatment is 1
Since this is done when a sheet is being coated, the masking step during coating can be omitted compared to when anti-corrosion treatment is performed after processing.
[実 施 例] 以下、本発明の実施例を図面を参照して説明する。[Example] Embodiments of the present invention will be described below with reference to the drawings.
第1図及び第2図は本発明の一実施例を示すもので、片
面にアルミニウム等をコーティングして防食処理を施こ
して防食処理層10bを有する母材としての1枚のプレ
ート10aに、平面的に見てコの字形の切込み部11を
多数個所に設け、該切込み部11により形成される舌片
12を上記防食処理層10bのある片面側へほぼ90度
の角度で折曲げ加工してガス通路形成用の凹凸を形成さ
せると共に多数の孔13を形成してカレントコレクター
10を構成する。FIGS. 1 and 2 show an embodiment of the present invention, in which one plate 10a as a base material has an anti-corrosion treatment layer 10b coated with aluminum or the like on one side, and A large number of U-shaped cut portions 11 are provided in a plan view, and the tongue piece 12 formed by the cut portions 11 is bent at an angle of approximately 90 degrees toward one side on which the anti-corrosion treatment layer 10b is located. The current collector 10 is constructed by forming unevenness for forming gas passages and forming a large number of holes 13.
電解質板1をカソード2とアノード3の両電極で両面か
ら挟むようにしであるセルCを積層してスタックとする
際に各セルCをセパレータを介して仕切る場合は、上記
構成としたカレントコレクター10の防食処理層10b
側とは反対側の面をカソード2、アノード3の各電極に
接触させるようにして折曲舌片12を相対向させ、両カ
レントコレクター10の上記折曲舌片12同士の間に、
従来のセパレータのセンタープレートとしてのセパレー
タプレート14を介在させるようにし、各セルC間の両
カレントコレクター10の折曲舌片12による凹凸によ
りカレントコレクター10とセパレータプレート14と
の間にガス通路15を形成させるようにする。When the cells C are stacked such that the electrolyte plate 1 is sandwiched between the cathode 2 and the anode 3 from both sides to form a stack, and each cell C is partitioned through a separator, the current collector 10 having the above structure is used. anti-corrosion treatment layer 10b
The bent tongue pieces 12 are made to face each other so that the opposite side thereof is in contact with each electrode of the cathode 2 and anode 3, and between the bent tongue pieces 12 of both current collectors 10,
A separator plate 14 is interposed as a center plate of a conventional separator, and a gas passage 15 is formed between the current collector 10 and the separator plate 14 by the unevenness of the bent tongue piece 12 of both current collectors 10 between each cell C. Let it form.
カソード2側に供給された酸化ガスOGは、カソード2
に接触するカレントコレクター10とセパレータプレー
ト14との間に形成されたガス通路15に供給された後
、カレントコレクター10の各社13を通してカソード
2へと導かれる。同様にアノード3側に導かれた燃料ガ
スFGは、アノード3に接触するカレントコレクター1
0とセパレータプレート14との間に形成されたガス通
路15に供給された後、カレントコレクター10の各社
13を通してアノード3に導かれる。The oxidizing gas OG supplied to the cathode 2 side
After being supplied to the gas passage 15 formed between the current collector 10 and the separator plate 14 that are in contact with the current collector 10 , it is led to the cathode 2 through the respective parts 13 of the current collector 10 . Similarly, the fuel gas FG guided to the anode 3 side is fed to the current collector 1 which contacts the anode 3.
After being supplied to the gas passage 15 formed between the current collector 10 and the separator plate 14, the gas is led to the anode 3 through the current collectors 13.
カソード2側での反応により得られた炭酸イオンCO3
−が電解質板1を通して7ノード3側へ導かれると、ア
ノード3で燃料ガスとの反応が行われるが、かかる反応
においてカソード2側とアノード3に生じた電位差によ
り電気が流されるが、カレントコレクター10は、電気
が流れることに利用される部分は防食処理がされていな
いので、電気の流れの障害となることはなく、又、防食
処理は1枚板のときに施こすことから、加工後に防食処
理を施こす場合の如きコーティングの際のマスキングの
工程を省略できる。Carbonate ion CO3 obtained by reaction on the cathode 2 side
When - is led to the 7 node 3 side through the electrolyte plate 1, a reaction with the fuel gas takes place at the anode 3. In this reaction, electricity is caused to flow due to the potential difference generated between the cathode 2 side and the anode 3, but the current collector 10, the parts used for electricity to flow are not anti-corrosion treated, so they do not interfere with the flow of electricity, and since the anti-corrosion treatment is applied to a single plate, it is difficult to prevent corrosion after processing. The masking step during coating, such as when applying anticorrosion treatment, can be omitted.
本発明の燃料電池においては、カレントコレクター10
の電気を流すときに利用する部分以外のところに防食処
理を施こしているので、作動温度が高く且つ腐食性の強
い溶融炭酸塩中にさらされていても、カレントコレクタ
ー10の腐食が防止されて、腐食による電解質中のリチ
ウムの消失を低減させることができて電池の寿命延長を
図ることが可能となる。In the fuel cell of the present invention, the current collector 10
Since anti-corrosion treatment is applied to the parts other than those used to conduct electricity, the current collector 10 is prevented from corrosion even when exposed to highly corrosive molten carbonate at high operating temperatures. As a result, the loss of lithium in the electrolyte due to corrosion can be reduced, making it possible to extend the life of the battery.
なお、本発明は、上記実施例のみに限定されるものでは
なく、たとえば、舌片12の折曲げ形状、孔13の形状
及びピッチ、等は図示以外のものとしてもよいこと、1
枚のプレートの片面に防食処理を施こした場合を示した
が、母材としての耐熱鋼とアルミニウムフェライト層と
を拡散接合させたクラツド鋼を加工してカレントコレク
ターとするようにしてもよいこと、その池水発明の要旨
を逸脱しない範囲内で種々変更を加え得ることは勿論で
ある。Note that the present invention is not limited to the above-described embodiments, and that, for example, the bent shape of the tongue piece 12, the shape and pitch of the hole 13, etc. may be other than those shown in the drawings;
Although the case in which anti-corrosion treatment is applied to one side of a single plate is shown, it is also possible to process clad steel in which heat-resistant steel as a base material and an aluminum ferrite layer are diffusion bonded to form a current collector. Of course, various changes can be made without departing from the gist of the invention.
[発明の効果]
以上述べた如く、本発明の燃料電池によれば、防食処理
を施こした1枚のプレートの多数個所に切込み部を設け
て、舌片を片面側へ折り曲げることによってガス通路を
形成させると共に多数の孔を設けた構成のカレントコレ
クターを、電極に接触させた状態で積層させるようにし
であるので、舌片を折り曲げることにより形成される凹
凸によりガス通路を形成させることができて、従来のセ
ンタープレートとコルゲート板とからなるセパレータに
おけるコルゲート板を省略でき、セパレータとしては1
枚のセパレータプレートのみでよくなり、製作コストを
低減できると共に、腐食によ、る電解質の消失を低減で
きて、電池の寿命を延ばすことができ、又、防食処理を
した後に加工することから、加工後に防食する場合の如
きマスキングの工程を省くことができ、更に、1枚板か
らなるため接触抵抗を低減させることができる、等の優
れた効果を奏し得る。[Effects of the Invention] As described above, according to the fuel cell of the present invention, the gas passages are formed by providing notches at multiple locations in one plate that has been subjected to anti-corrosion treatment and by bending the tongue piece to one side. Since the current collectors are stacked in contact with the electrodes and have a large number of holes, gas passages can be formed by the unevenness formed by bending the tongues. Therefore, the corrugated plate in the conventional separator consisting of a center plate and a corrugated plate can be omitted, and the separator only has one
Only one separator plate is required, which reduces production costs, reduces the loss of electrolyte due to corrosion, and extends battery life.Also, since it is processed after anti-corrosion treatment, It is possible to omit the masking step required for corrosion prevention after processing, and furthermore, since it is made of a single plate, it can exhibit excellent effects such as being able to reduce contact resistance.
第1図は本発明の燃料電池の一実施例を示す部分の切断
側面図、第2図は本発明の燃料電池におけるカレントコ
レクターの斜視図、第3図は従来の燃料電池の一例を示
す切断面図である。
1・・・電解質板、2・・・カソード、3・・・アノー
ド、4・・・セパレータ、10・・・カレントコレクタ
ー、10a・・・プレート、10b・・・防食処理層、
11・・・切込み部、12・・・舌片、13・・・孔、
14・・・セパレータプレート、15・・・ガス通路、
OG・・・酸化ガス、FG・・・燃料ガス。FIG. 1 is a cutaway side view of a portion showing an embodiment of the fuel cell of the present invention, FIG. 2 is a perspective view of a current collector in the fuel cell of the present invention, and FIG. 3 is a cutaway view of an example of a conventional fuel cell. It is a front view. DESCRIPTION OF SYMBOLS 1... Electrolyte plate, 2... Cathode, 3... Anode, 4... Separator, 10... Current collector, 10a... Plate, 10b... Anticorrosion treatment layer,
11... Notch portion, 12... Tongue piece, 13... Hole,
14...Separator plate, 15...Gas passage,
OG...oxidizing gas, FG...fuel gas.
Claims (1)
切込み部を設け、該切込み部の舌片を防食処理した片面
側へ折り曲げ加工して凹凸部を形成してなるカレントコ
レクターを構成し、電解質板の両面をカソードとアノー
ドの両電極で挟んでカソード側に酸化ガスを、又、アノ
ード側に燃料ガスをそれぞれ供給するようにしてあるセ
ルの上記両電極に、上記カレントコレクターの反折曲舌
片側をそれぞれ接触させ、且つセル間の各カレントコレ
クターの各折曲舌片同士の間にセパレータプレートを介
在させた構成としてなることを特徴とする燃料電池。(1) A current collector is constructed by providing notches at multiple locations on a single plate that has been treated with anti-corrosion treatment, and bending the tongues of the notches toward one side that has been treated with anti-corrosion treatment to form uneven portions. The electrolyte plate is sandwiched between the cathode and anode electrodes so that oxidizing gas is supplied to the cathode side and fuel gas is supplied to the anode side. 1. A fuel cell characterized in that one side of the bent tongues are in contact with each other, and a separator plate is interposed between the bent tongues of each current collector between cells.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1218534A JPH0384867A (en) | 1989-08-28 | 1989-08-28 | Fuel cell |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1218534A JPH0384867A (en) | 1989-08-28 | 1989-08-28 | Fuel cell |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0384867A true JPH0384867A (en) | 1991-04-10 |
Family
ID=16721435
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1218534A Pending JPH0384867A (en) | 1989-08-28 | 1989-08-28 | Fuel cell |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0384867A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006107968A (en) * | 2004-10-07 | 2006-04-20 | Toyota Motor Corp | Gas passage forming member for fuel cell, and fuel cell |
JP2012248460A (en) * | 2011-05-30 | 2012-12-13 | Nissan Motor Co Ltd | Fuel cell unit and fuel cell stack |
-
1989
- 1989-08-28 JP JP1218534A patent/JPH0384867A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006107968A (en) * | 2004-10-07 | 2006-04-20 | Toyota Motor Corp | Gas passage forming member for fuel cell, and fuel cell |
JP4639744B2 (en) * | 2004-10-07 | 2011-02-23 | トヨタ自動車株式会社 | Fuel cell |
JP2012248460A (en) * | 2011-05-30 | 2012-12-13 | Nissan Motor Co Ltd | Fuel cell unit and fuel cell stack |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US7745035B2 (en) | Separator and fuel cell using thereof | |
JPH08222237A (en) | Separator for fuel cell | |
JP5226431B2 (en) | Fuel cell stack | |
US5811202A (en) | Hybrid molten carbonate fuel cell with unique sealing | |
JPS61216257A (en) | Separator for fuel cell | |
JP2004087311A (en) | Fuel cell stack and metallic separator for for fuel cell stack | |
JP2000133282A (en) | Separator for solid polymer electrolyte fuel cell | |
JP2002367624A (en) | Fuel cell | |
JPH0384867A (en) | Fuel cell | |
JPS625569A (en) | Molten carbonate type fuel cell stack | |
JP6825084B2 (en) | Fuel cell | |
JPH0652868A (en) | Separator masking material for molten carbonate fuel cell and manufacture thereof | |
JPS5998473A (en) | Molten carbonate type fuel cell | |
JP2822457B2 (en) | Fuel cell separator and method of manufacturing the same | |
JPS63181271A (en) | Fused carbonate fuel cell | |
JPH07153472A (en) | Current collecting plate for fuel cell | |
JPH0414854Y2 (en) | ||
JPS622460A (en) | Molten carbonate type fuel cell | |
JPS62122070A (en) | Molten carbonate fuel cell stack | |
JPH0346951B2 (en) | ||
JPH0418433B2 (en) | ||
JP2024515124A (en) | Separator plate assembly for fuel cells with variable flow path patterning - Patents.com | |
JPS63226885A (en) | Fuel cell | |
JP3110902B2 (en) | Fuel cell | |
JPH0426068A (en) | Fuel cell |